CN103372328A - Rotating packed bed for dual-phase extraction - Google Patents
Rotating packed bed for dual-phase extraction Download PDFInfo
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- CN103372328A CN103372328A CN2012101260721A CN201210126072A CN103372328A CN 103372328 A CN103372328 A CN 103372328A CN 2012101260721 A CN2012101260721 A CN 2012101260721A CN 201210126072 A CN201210126072 A CN 201210126072A CN 103372328 A CN103372328 A CN 103372328A
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- packed bed
- packing
- distributor
- phase
- rotary packed
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- 238000000605 extraction Methods 0.000 title claims abstract description 39
- 238000012856 packing Methods 0.000 claims abstract description 42
- 239000000945 filler Substances 0.000 claims description 42
- 239000000463 material Substances 0.000 claims description 15
- -1 Merlon Substances 0.000 claims description 8
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 8
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 8
- 229910001369 Brass Inorganic materials 0.000 claims description 4
- 229910001209 Low-carbon steel Inorganic materials 0.000 claims description 4
- 229920000877 Melamine resin Polymers 0.000 claims description 4
- 239000004642 Polyimide Substances 0.000 claims description 4
- 239000010951 brass Substances 0.000 claims description 4
- 239000003822 epoxy resin Substances 0.000 claims description 4
- 229920001568 phenolic resin Polymers 0.000 claims description 4
- 229920000647 polyepoxide Polymers 0.000 claims description 4
- 229920005644 polyethylene terephthalate glycol copolymer Polymers 0.000 claims description 4
- 229920001721 polyimide Polymers 0.000 claims description 4
- 239000004800 polyvinyl chloride Substances 0.000 claims description 4
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 239000006096 absorbing agent Substances 0.000 claims description 3
- 238000013016 damping Methods 0.000 claims description 3
- 230000035939 shock Effects 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 2
- 239000000284 extract Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 13
- 239000002994 raw material Substances 0.000 abstract description 10
- 230000009471 action Effects 0.000 abstract description 2
- 230000002349 favourable effect Effects 0.000 abstract 1
- 230000002093 peripheral effect Effects 0.000 abstract 1
- 238000009827 uniform distribution Methods 0.000 abstract 1
- 239000012071 phase Substances 0.000 description 44
- 239000007921 spray Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000622 liquid--liquid extraction Methods 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 235000019774 Rice Bran oil Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000008165 rice bran oil Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
The invention relates to a rotating packed bed for dual-phase extraction. The rotating packed bed comprises a rotor, a feed distributor and a shell, wherein the rotor comprises a packing support plate and silk screen packing, and the silk screen packing is respectively filled into a packing bracket by two layers and then fixed on the packing support plate and is in positioned connection with a rotating shaft through bonds; the feed distributor comprises a raw material feed distributor and heavy and light phase extractant feed distributors, wherein the raw material feed distributor is positioned in a gap between the two layers of packing, the heavy and light phase feed distributors are respectively positioned on the outer side of the outer layer of the packing and the inner side of the inner layer of the packing, and a packed bed bottom plate is provided with a light phase outlet pipe and a heavy phase outlet pipe which are partitioned by a baffle plate. The rotating packed bed is simple in structure and is used for realizing favorable axial and peripheral uniform distribution of liquid under the action of centrifugal force and realizing countercurrent sufficient contact between liquid, thereby improving the extraction efficiency.
Description
Technical field
The present invention relates to a kind of rotary packed bedly, be specifically related to a kind of rotary packed bed for two-phase extraction.
Background technology
Rotary packed bed is a kind of novel device of strengthening chemical process, and with respect to traditional extraction equipment, rotary packed bed simple in structure, volume is little, and operational efficiency is high, and energy consumption is lower and applied widely, has obvious advantage aspect the mass transfer extraction.
Patent CN201752626U discloses a kind of many rotational flow dust-removings of hypergravity desulfurization multifunctional device, patent CN201752587U discloses a kind of high-gravity rotating bed with multi-layer cylinder formula rotary liquid distributor, patent CN201752586U discloses a kind of high-gravity rotating bed with the coiled rotary liquid distributor, and patent CN201108754Y discloses a kind of multi-Spraying Rotating Packed Bed.More than these patents the revolving bed of several different structures is disclosed respectively, these revolving beds have been successfully applied to the process industrials such as reaction, absorption, desorb.
The two-phase abstraction technique is a kind of liquid-liquid extraction isolation technics commonly used, because it has preferably effect of extracting, biochemistry and biological chemical field have been widely used in, patent CN102177243A discloses a kind of method of utilizing the two-phase extractive fermentation to produce ethanol, and patent CN101984028A discloses a kind of high oryzanol rice bran oil two-phase extraction de-acidification refining technology.Existing two-phase extraction equipment mainly is turntable extracting tower, and this equipment rotating speed is slow and volume is larger, and extraction yield is low.
Existing rotary packed bedly be successfully applied to a plurality of fields, but its individual layer filling-material structure is restricted its application in the two-phase extraction; And existing two-phase extraction equipment have the cost height, bulky, extraction rate is slow, the much lower weak point of extraction efficiency.
Summary of the invention
The present invention is directed to the technical problem that existing rotary packed bed structure can not satisfy the two-phase extraction, proposed a kind of Novel rotary packed bed for the two-phase extraction; Described Novel rotary packed bed can be realized two-phase extraction, have simple in structure, extraction efficiency is high, the characteristics of good separating effect.The present invention has realized the liquid-liquid extraction between two kinds of extractants of a kind of two-phase raw material, utilize simultaneously rotary packed bed High Rotation Speed, liquid forms the as thin as a wafer this inherent characteristic of liquid film reduction resistance to mass tranfer at filling surface, make the weight liquid phase under the effect of centrifugal force, obtain the even distribution of good axial and circumferential, realize the abundant contact between liquid, thereby promoted extraction efficiency.
Two-phase extraction of the present invention is rotary packed bed, comprise filler rotor, feed distributor and housing, described filler rotor comprises main shaft, packing support plate, filler frame and wire packing, wire packing is divided into two-layer, be fixed on the packing support plate after putting into respectively the filler basket, and be located by connecting by key and rotating shaft; Described feed distributor comprises feed distribution device and light, the heavy phase distributor, the feed distribution device is between two-layer filler space, light phase distributor is positioned at the filler outside, outer ring, it is inboard that the heavy phase distributor is positioned at the inner ring filler, light phase distributor is fixed on the rotary packed bed cylindrical shell, heavy phase distributor and feed distribution device are fixed on the rotary packed bed base plate, described feed distributor is equipped with four perforate arms and evenly distributes ringwise and every layer of feed-inputing branched pipe all is provided with independent T-Ring and is connected and fixed, two kinds of extractants and raw material spray into filler by distributor perforate separately respectively, contact mass transfer in filler, feed distribution device (10) is two both sides open double-faced, and light phase distributor (6) is inside one-sided opening, the outside one-sided opening of heavy phase distributor.Specifically shown in Fig. 1～4.
Described wire packing material has stainless steel, mild steel, brass or macromolecular material such as polyvinyl chloride, Merlon, polytetrafluoroethylene (PTFE), PETG, epoxy resin, phenoplasts, polyimides or melamine formaldehyde resin, and concrete material requires to select according to concrete operating temperature and medium; Described wire packing is loaded in the described filler basket, is bolted on the packing support plate; The structure of described filler frame determines what by the wire packing that loads; Described packing support plate is connected with rotating shaft, and the rotating shaft rotating speed is controlled in the 3000r/min scope; Preferred 1200～2000r/min, rotating shaft and rotary packed bed base plate, upper plate junction are provided with sealing device, and described sealing device adopts the Double End movable sealing.
Double-deck filling-material structure has also guaranteed the contact area of storeroom simultaneously for the layout of feed distributor provides the space; Two kinds of extractants and material liquid adopt the counter current contacting mass transfer; Lower plate arranges back-up ring, and heavy out pipe and light phase export pipe are separated, and makes extraction product realize better separating; Three feed distributors support with support bar or bracing ring; The present invention arranges supporting leg in the packed bed bottom, and damping shock absorber is installed, and reduces the unbalance dynamic of filler rotor and damages to the vibrations that equipment causes, and has prolonged the service life of equipment; Rotary packed bed all opening-nozzles all adopt connection by metal hose.
As the improvement on the basis of the double-deck filler of the present invention, a kind of Novel rotary packed bed structure with four layers of filler for the two-phase extraction is provided, the described rotary packed bed four layers of filling-material structure that have, add respectively one deck filler in the outside of light phase feed distributor and the inboard of heavy phase feed distributor, form three packing layer cracks and a center driving cylinder ring, raw material feed distributor arm is positioned at place, intermediate filler layer crack, and two kinds of extractant distributors lay respectively at outer packing layer crack and internal layer packing layer crack; Two kinds of extractants and material liquid adopt the counter current contacting mass transfer.Four layers of filling-material structure have increased the extraction distributed area of weight phase, prevent that the part extractant can not be injected in the packing layer, has improved the utilization rate of extractant; Having added inside and outside two-layer filler makes material liquid mix more even in filler with two kinds of extractants, improve mass-transfer efficiency, improve extraction yield, described wire packing (22,23) material is stainless steel, mild steel, brass, polyvinyl chloride, Merlon, polytetrafluoroethylene (PTFE), PETG, epoxy resin, phenoplasts, polyimides or melamine formaldehyde resin, specifically shown in Fig. 5,6.
Description of drawings
Fig. 1 the present invention has the rotary packed bed structural representation of double-deck filler.
The two-layer filler of Fig. 2 the present invention schematic diagram of arranging.
The rotary packed bed feed distributor position of opening of Fig. 3 the present invention schematic diagram of arranging.
The rotary packed bed base schematic diagram of Fig. 4 the present invention.
Fig. 5 the present invention has the rotary packed bed structural representation of four layers of filler.
Four layers of filler of Fig. 6 the present invention schematic diagram of arranging.
The specific embodiment
Further specify the present invention below in conjunction with the drawings and specific embodiments.
Provide the first embodiment of the present invention shown in Fig. 1～4, a kind ofly can be used for the rotary packed bed of two-phase extraction, described revolving bed comprises housing, rotor and feed distributor.Rotary packed bed below is provided with supporting leg (19) and damping shock absorber (20).
Raw material enters feed distributor 10 by feed(raw material)inlet pipe 12, and is sprayed in the wire packing by the staggered spray orifice 18 in feed distribution device 10 both sides; Heavy phase enters heavy phase distributor 13 by heavy liquid inlet pipe 11, and sprays into packing layer by the spray orifice 18 that deviates from the filler central side; Gently enter light phase distributor 6 by light phase inlet tube 7, and spray into packing layer by the spray orifice near the filler central side.The filler rotor 1 powerful centrifugal force that High Rotation Speed produces under the motor 21 that links to each other by belt with main shaft 5 drives, so that enter material liquid in the packing layer along the filler radial diffusion, radially outward throw away along filler behind heavy phase raw material and the heavy phase extractant counter current contacting mass transfer, heavy phase is collected by cylindrical shell 16 inwalls after throwing away the filler rotor, flow into baffle plate 8 exterior annular zone, heavy out pipe 14 flows out from the rotary packed bed base plate 15 at last; Because the ring packing center produces negative pressure, light phase raw material with gently be attracted to the filler center after the phase extractant contact mass transfer, radially to the ring packing central motion, move to inflow baffle plate 8 medial region behind the ring packing center, flow out from rotary packed bed base plate 15 light phase export pipes 9 at last.
Provide the second embodiment of the present invention shown in Fig. 5,6, a kind of Novel rotary packed bed with four layers of filler for the two-phase extraction, described revolving bed comprises filler rotor, feed distributor and housing.
This example increases outer packing layer 22 and internal layer packing layer 23 on example 1 basis, the heavy phase extractant of heavy phase distributor 26 ejections outwards moves under the powerful centrifugal action of filler rotor, and the light phase extractant of light phase distributor 24 ejections inwardly moves; Material liquid is distributed in the packing layer by feed distribution device 25 spouts, realizes the contact mass transfer extraction of the adverse current between two-phase extractant and the raw material.At last, heavy phase carries out evenly throwing away the filler rotor after the distribution extraction again in outer filler, flows out from heavy out after being collected by barrel; Light carrying out in the internal layer filler again flows into the filler center ring after the evenly extraction, falls on the base plate and flowed out by light phase export.
Claims (10)
1. a two-phase extraction is rotary packed bed, comprise filler rotor (1), feed distributor (6,10,13) and cylindrical shell (16), it is characterized in that described filler rotor (1) comprises rotating shaft (5), packing support plate (2), filler frame (3) and wire packing (4), wire packing is two-layer, be fixed in (2) on the packing support plate after putting into respectively filler basket (3), described feed distributor comprises feed distribution device (10) and light, heavy phase distributor (6,13), feed distribution device (10) is between two-layer filler, light phase distributor (6) is positioned at the filler outside, outer ring, it is inboard that heavy phase distributor (13) is positioned at the inner ring filler, and the packed bed base plate is provided with by baffle plate (8) separates light phase export pipe (14) and heavy out pipe (9).
2. two-phase extraction according to claim 1 is rotary packed bed, it is characterized in that described feed distributor (6,10,13) is equipped with four perforate arms, and evenly distributes ringwise.
3. two-phase extraction according to claim 1 is rotary packed bed, it is characterized in that rotary packed bed below is provided with supporting leg (19) and damping shock absorber (20).
4. two-phase extraction according to claim 1 is rotary packed bed, it is characterized in that described wire packing (6) material is stainless steel, mild steel, brass, polyvinyl chloride, Merlon, polytetrafluoroethylene (PTFE), PETG, epoxy resin, phenoplasts, polyimides or melamine formaldehyde resin.
5. two-phase extraction according to claim 1 is rotary packed bed, it is characterized in that described feed distribution device (10) is two both sides open double-faced, and light phase distributor (6) is inside one-sided opening, the outside one-sided opening of heavy phase distributor.
6. two-phase extraction according to claim 2 is rotary packed bed, it is characterized in that described feed distributor (6,10,13) feed-inputing branched pipe has independent T-Ring (17) to be connected and fixed.
7. two-phase extraction according to claim 1 is rotary packed bed, it is characterized in that described rotary packed bed opening-nozzle (7,11,12) all adopts metal hose.
8. a two-phase extraction is rotary packed bed, it is characterized in that the interior outside that extracts rotary packed bed wire packing in two-phase claimed in claim 1 respectively adds one deck wire packing (22,23), wire packing is four layers, form three packing layer cracks and a center driving cylinder ring, feed distribution device (25) is positioned at the intermediate filler layer crack, light phase distributor (24) is positioned at outer packing layer crack, and heavy phase distributor (26) is positioned at internal layer packing layer crack.
9. two-phase extraction according to claim 8 is rotary packed bed, it is characterized in that described feed distributor (24,25,26) is equipped with four perforate arms, and evenly distributes ringwise.
10. two-phase extraction according to claim 8 is rotary packed bed, it is characterized in that described wire packing (22,23) material is stainless steel, mild steel, brass, polyvinyl chloride, Merlon, polytetrafluoroethylene (PTFE), PETG, epoxy resin, phenoplasts, polyimides or melamine formaldehyde resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210126072.1A CN103372328B (en) | 2012-04-17 | 2012-04-17 | A kind of two-phase extraction is rotary packed bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210126072.1A CN103372328B (en) | 2012-04-17 | 2012-04-17 | A kind of two-phase extraction is rotary packed bed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103372328A true CN103372328A (en) | 2013-10-30 |
| CN103372328B CN103372328B (en) | 2015-09-30 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201210126072.1A Expired - Fee Related CN103372328B (en) | 2012-04-17 | 2012-04-17 | A kind of two-phase extraction is rotary packed bed |
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| Country | Link |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941246A (en) * | 2015-04-21 | 2015-09-30 | 昆明理工大学 | Impinging stream super-gravity liquid-liquid extractor |
| CN108905270A (en) * | 2018-08-30 | 2018-11-30 | 安徽珠峰生物科技有限公司 | A kind of extraction equipment |
| CN111405933A (en) * | 2018-08-21 | 2020-07-10 | 株式会社Lg化学 | Solid phase extraction method using micro device |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1499554A (en) * | 1975-09-11 | 1978-02-01 | Seliverstov K | Centrifugal liquid-liquid extractor |
| JPH03103A (en) * | 1989-05-26 | 1991-01-07 | Mitsubishi Kakoki Kaisha Ltd | Centrifugal extractor |
| US6440054B1 (en) * | 2000-09-18 | 2002-08-27 | George M. Galik | Apparatus for liquid-liquid extraction |
| CN1631482A (en) * | 2004-11-12 | 2005-06-29 | 高根树 | Extracting device |
| CN101036841A (en) * | 2007-02-02 | 2007-09-19 | 浦华控股有限公司 | Down-transmission type centrifugal extractor for the chemical industry operation |
| CN200977420Y (en) * | 2006-12-02 | 2007-11-21 | 张春新 | Single level centrifugal extracting machine |
| CN102078704A (en) * | 2010-12-31 | 2011-06-01 | 玄浩 | Centrifugal extractor |
-
2012
- 2012-04-17 CN CN201210126072.1A patent/CN103372328B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1499554A (en) * | 1975-09-11 | 1978-02-01 | Seliverstov K | Centrifugal liquid-liquid extractor |
| JPH03103A (en) * | 1989-05-26 | 1991-01-07 | Mitsubishi Kakoki Kaisha Ltd | Centrifugal extractor |
| US6440054B1 (en) * | 2000-09-18 | 2002-08-27 | George M. Galik | Apparatus for liquid-liquid extraction |
| CN1631482A (en) * | 2004-11-12 | 2005-06-29 | 高根树 | Extracting device |
| CN200977420Y (en) * | 2006-12-02 | 2007-11-21 | 张春新 | Single level centrifugal extracting machine |
| CN101036841A (en) * | 2007-02-02 | 2007-09-19 | 浦华控股有限公司 | Down-transmission type centrifugal extractor for the chemical industry operation |
| CN102078704A (en) * | 2010-12-31 | 2011-06-01 | 玄浩 | Centrifugal extractor |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941246A (en) * | 2015-04-21 | 2015-09-30 | 昆明理工大学 | Impinging stream super-gravity liquid-liquid extractor |
| CN104941246B (en) * | 2015-04-21 | 2016-09-21 | 昆明理工大学 | A kind of percussion flow hypergravity liquid-liquid extraction device |
| CN111405933A (en) * | 2018-08-21 | 2020-07-10 | 株式会社Lg化学 | Solid phase extraction method using micro device |
| CN111405933B (en) * | 2018-08-21 | 2021-12-07 | 株式会社Lg化学 | Solid phase extraction method using micro device |
| US11260319B2 (en) | 2018-08-21 | 2022-03-01 | Lg Chem, Ltd. | Solid phase extraction method using micro device |
| CN108905270A (en) * | 2018-08-30 | 2018-11-30 | 安徽珠峰生物科技有限公司 | A kind of extraction equipment |
Also Published As
| Publication number | Publication date |
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| CN103372328B (en) | 2015-09-30 |
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